EP0468621B1

EP0468621B1 - Pilot valve for control valves and method of operation

Info

Publication number: EP0468621B1
Application number: EP91304425A
Authority: EP
Inventors: Michael D. Mcneely
Original assignee: Keystone International Holdings Corp
Current assignee: Keystone International Holdings Corp
Priority date: 1990-06-04
Filing date: 1991-05-16
Publication date: 1996-04-24
Anticipated expiration: 2011-05-16
Also published as: DE69118983T2; KR920021908A; CA2042787A1; DE69118983D1; JPH04231784A; MX173879B; KR100194854B1; US5027852A; EP0468621A1; JP3043466B2

Description

BACKGROUND OF THE INVENTION

This invention relates to a pilot valve for a control valve in a main flow line, and more particularly to such a pilot valve and method of operation utilizing a fluid source separate from the process fluid in the main flow line.
Heretofore, it has been common to utilize only the process fluid in the main flow line being sensed for the operation of the pilot valve for the main control valve. Oftentimes, the process fluid in the main flow line contains foreign matter which may clog or restrict flow passages, and bind or space opposed sealing and sliding surfaces. While pilot valves may be successfully used in such applications, an adequate maintenance and cleaning of the pilot valve is required in order to ensure that the pilot valve is fully functional. Continuous and frequent maintenance of such pilot valves is an undesirable feature.

SUMMARY OF THE INVENTION

The present invention is directed to a pilot valve for a control valve in a main flow line in which the process fluid in the flow line is sensed by the pilot valve but is isolated from critical working parts of the pilot valve and the associated main control valve including the flow passages, the seating and sealing surfaces of the pilot valve, and the dome chamber of the main valve. A separate auxiliary source of a clean fluid, such as a high pressure gas, is utilized for contact with the dome chamber of the main valve and the seating and sealing surfaces of the pilot valve thereby exposing such critical operating members only to a clean dry gas. A fluid pressure regulator is provided for the pressurized gas source to supply gas at a predetermined constant fluid pressure to the pilot valve.
The pilot valve has a fluid inlet sensing chamber in fluid communication with process fluid from the main flow line, and a separate fluid inlet supply chamber in fluid communication with a separate auxiliary pressurized fluid source isolated from the process fluid. An intermediate fluid chamber in fluid communication with the dome chamber in the control valve is adapted to be in selective fluid communication with the fluid inlet supply chamber for the supply of fluid to the dome chamber upon the reaching of a predetermined low fluid pressure in the process fluid as sensed in the sensing chamber. The intermediate fluid chamber is also adapted to be in selective fluid communication to atmosphere for the release of fluid from the dome chamber upon the reaching of a predetermined high fluid pressure in the process fluid as sensed in the sensing chamber. Suitable valving or valve means responsive to the process fluid pressure in the sensing chamber is provided for selectively placing the intermediate chamber in fluid communication with the fluid inlet supply chamber containing the auxiliary fluid at a predetermined low fluid pressure in the process fluid, and for selectively placing the intermediate chamber in fluid communication with an exhaust chamber at a predetermined high fluid pressure in the process fluid. The process fluid and the auxiliary fluid source remain isolated from each other during the entire operation of the pilot valve.
It is an object of the invention to provide a pilot valve for a control valve in which the sensed process fluid is isolated from the dome chamber of the control valve and the seating and sealing surfaces of the pilot valve.
It is another object of the present invention to provide a pilot valve for a control valve in a main flow line with the pilot valve having an inlet sensing chamber for sensing the process fluid in the main flow line and a separate auxiliary fluid inlet supply chamber having a separate auxiliary fluid for operation of the pilot valve.
It is an additional object of the invention to provide an improved method of operation of a pilot valve by utilizing a separate auxiliary source of fluid sensing the process fluid in the main flow line and having a separate auxiliary fluid for operation of the pilot valve.
A further object of the invention is to provide such a pilot valve for a control valve in which an auxiliary pressurized gas source separate from the sensed process fluid is supplied to the pilot valve at a predetermined constant pressure for operation thereof and is in selective fluid communication with the dome chamber of the control valve.
According to the invention there is therefore provided a safety relief system for a pressure vessel having a safety relief valve in a main flow line from the pressure vessel, the safety relief valve including a reciprocable piston type valve member mounted in the flow line in a normally closed position and a dome chamber adjacent an end of the reciprocable valve member;

a pilot valve having a fluid inlet sensing chamber for process fluid from the flow line and a fluid inlet supply chamber for an auxiliary fluid separate from said process fluid;
means providing fluid communication between said main flow line and said fluid inlet sensing chamber;
means to supply an auxiliary fluid to said fluid inlet supply chamber at a predetermined fluid pressure;
a separate fluid chamber in said pilot valve in fluid communication with said dome chamber;
an exhaust to atmosphere from said separate fluid chamber;
a movable fluid sensing member in said sensing chamber exposed to said process fluid and responsive to pressure changes in said main flow line;
and
valve means between said separate fluid chamber and said exhaust for normally blocking fluid communication between said separate fluid chamber and said supply chamber;
said valve means being responsive to movement of said fluid sensing member at a predetermined fluid pressure of said process fluid for permitting fluid communication between said separate fluid chamber and said exhaust for reducing fluid pressure in said dome chamber upon the reaching of a predetermined fluid pressure in said process fluid.

Preferably, the safety relief system comprises additional valve means between said fluid inlet supply chamber for said auxiliary fluid supply and said separate fluid chamber normally blocking fluid communication between said separate fluid chamber and said inlet supply chamber;

said valve means being responsive to movement of said fluid sensing member at a predetermined fluid pressure of said process fluid for permitting fluid communication between said fluid supply inlet supply chamber and said separate fluid chamber to provide an auxiliary fluid supply to said separate fluid chamber and said dome chamber at a predetermined pressure reached by said process fluid.

It is preferred that the movable fluid sensing member comprises a diaphragm and a piston connected to said diaphragm for movement therewith.
It is also preferred that the valve means comprises a spool valve member responsive to said piston for opening upon a predetermined fluid pressure of said process fluid to permit fluid communication between said dome chamber and said exhaust for reducing fluid pressure in said dome chamber to permit opening of said safety relief valve upon the reaching of a predetermined high fluid pressure in said process fluid.
According to the invention there is also provided a method of operating a pilot valve for a control valve in a main flow line in a safety relief system which comprises the following steps;

providing a fluid inlet sensing chamber in the pilot valve in fluid communication with process fluid in the main flow line;
providing a fluid inlet supply chamber in said pilot valve in fluid communication with an auxiliary fluid supply isolated from said process fluid;
providing a source of auxiliary fluid for said fluid inlet supply chamber;
providing an intermediate fluid chamber in fluid communication with a dome chamber in the control valve and in selective fluid communication with said fluid inlet supply chamber;
providing a fluid exhaust chamber in selective fluid communication with said intermediate fluid chamber for reducing the fluid pressure in said dome chamber;
and
providing valving between said intermediate fluid chamber and said exhaust chamber responsive to changes in process fluid pressure in said fluid inlet sensing chamber and blocking fluid communication between said intermediate fluid chamber and said exhaust chamber during normal operation, said valving permitting fluid communication between said intermediate chamber and said exhaust chamber upon the reaching of a predetermined high fluid pressure in said fluid inlet sensing chamber for reducing fluid pressure in said dome chamber.

It is preferred that the method of operating the pilot valve further includes the steps of

providing additional valving betwen said intermediate fluid chamber and said fluid inlet supply chamber responsive to changes in process fluid pressure in said fluid inlet sensing chamber and blocking fluid communication between said intermediate fluid chamber and said fluid inlet supply chamber during normal operation, said additional valving permitting fluid communication between said intermediate chamber and said fluid inlet chamber upon the reaching of a predetermined low fluid pressure in said fluid inlet sensing chamber thereby to provide auxiliary fluid pressure to said dome chamber for said control valve.

Other objects, advantages, and features of the invention will become more apparent after referring to the following specification and drawings.

BRIEF DESCRIPTION OF THE DRAWINGS

Figure 1 is a cross sectional view, partly schematic, of a system for controlling a pressure relief valve in a main flow line and including the improved pilot valve of the present invention with a separate auxiliary fluid source;
Figure 2 is an enlarged fragment of the improved pilot valve of Figure 1 showing the pilot valve in a normal operating condition with the spool valve member in seated position blocking fluid communication with the intermediate fluid chamber of the pilot valve and the dome chamber of the pressure relief valve;
Figure 3 is an enlarged fragment of the pilot valve similar to Figure 2 but showing the pilot valve exposed to a predetermined high process fluid pressure of the main flow line with the intermediate fluid chamber and the dome chamber of the pressure relief valve in fluid communication to atmosphere to reduce the fluid pressure in said dome chamber; and
Figure 4 is an enlarged fragment of the pilot valve similar to Figures 2 and 3 but showing the pilot valve exposed to a predetermined low process fluid pressure of the main flow line with the intermediate fluid chamber in fluid communication with the inlet fluid supply chamber for the auxiliary fluid source to supply auxiliary fluid to the dome chamber of the pressure relief valve for increasing the fluid pressure therein.

DESCRIPTION OF THE INVENTION

Referring now to the drawings for a better understanding of this invention, and more particularly to Figure 1 in which the safety system including the improved pilot valve of this invention is illustrated, a pressure vessel or tank is partially shown at 10 and has an outlet extending therefrom including an upper flange 12. A main pressure relief valve indicated generally at 14 has a valve body 16 including a lower flange 18 connected to flange 12 by suitable nut and bolt combinations indicated generally at 20.
Valve body 16 includes a valve chamber 22 with an inlet flow passage 24 and an outlet flow passage 26 communicating therewith. A piston type relief valve member shown generally at 28 is mounted within valve chamber 22 for reciprocable movement and has an inner face 29 forming a seat for seating against an annular seat 30 about inlet flow passage 24. Inner face 29 of valve member 28 is normally exposed to process fluid from inlet flow passage 24 and tank 10 and has a rear face 34 exposed to fluid pressure from a dome chamber 36. The area of inner face 29 exposed to fluid pressure from inlet flow passage 24 in closed position is less than the area of outer face 34 exposed to fluid pressure in dome chamber 36. Thus, a fluid pressure differential area is provided between faces 29 and 34 and a fluid pressure in dome chamber 36 lower than the fluid pressure in inlet flow passage 24 will maintain valve member 28 in seated position on seat 30.
The improved pilot valve forming the present invention is generally shown at 40 and has a valve body 42 defining a lower body portion 44 and an upper body portion 46. Lower body portion 44 has an upper flange 48 and upper body portion 46 has a lower flange 50 which clamp a sensing diaphragm 52 therebetween. A spring 54 urges diaphragm 52 downwardly and an adjusting screw 56 may be manually actuated to adjust the pressure exerted by spring 54. An exhaust to atmosphere for upper body portion 46 is provided at 58.
Lower body portion 44 defines a fluid inlet sensing chamber 60 adjacent sensing diaphragm 52 in fluid communication through sensing line 62 with inlet flow passage 24 containing process fluid. Thus, inlet sensing chamber 60 is exposed to process fluid from tank 10 at all times. Lower body portion 44 has a large diameter central bore portion 66 adjacent fluid sensing chamber 60 and a small diameter end bore portion 68 communicating with bore portion 66. A piston shown generally at 70 is secured to diaphragm 52 for movement therewith and is mounted for reciprocable movement within enlarged diameter bore portion 66. Piston 70 has a large diameter internal bore portion 72 forming a fluid inlet supply chamber and a small diameter entrance bore portion 74 communicating with large diameter internal bore portion 66.
A spool valve member shown generally at 76 has a central bore 78 extending therethrough and defines a large diameter lower end portion 80 and a reduced diameter portion 82 extending from end portion 80. End portion 80 fits within bore 68 and reduced diameter portion 82 fits within bore 68 and extends through small diameter entrance bore 74 of piston 70. An annular space 84 within bore 68 is provided about reduced diameter bore portion 82 and an annular space 86 within entrance bore 74 of piston 70 is provided about reduced diameter portion 82. Spool valve member 76 has an upper end flange 88 with an O-ring seal 90 about its inner surface adapted to seat on an annular seat 92 about small diameter bore portion 74. An intermediate flange 94 has an O-ring seal 96 about its inner surface adapted to seal on seat 98 extending about the upper end of bore 68. A relatively light spring 100 is biased between piston 70 and upper end flange 88 of spool valve member 76 to urge spool valve member 76 to a normal seated position as shown in Figure 2 with O-ring 90 in seating engagement on seat 92 and O-ring 96 in seating engagement on seat 98. An exhaust fluid passage 102 extends from bore 68 through body portion 44 to atmosphere to provide a bleed or exhaust chamber.
As shown in the position of Figures 1 and 2 with O- rings 90 and 96 in seated position on respective seats 92 and 98, a fluid inlet supply chamber 72 is formed by the internal bore of piston 70, an intermediate fluid chamber 104 is formed in enlarged bore portion 66 adjacent piston 70 which is in continuous fluid communication with dome chamber 36 through dome line 106 from chamber 104 to dome chamber 36, and a fluid outlet chamber or exhaust chamber is formed by exhaust fluid passage 102 in bore portion 68 in fluid communication to atmosphere. To provide a clean supply of fluid to inlet chamber 72, intermediate chamber 104, and dome chamber 36, a source or supply of high pressure gas such as nitrogen, is provided at 107. A pressure reducing regulator 108 adjacent fluid source 107 provides a constant predetermined pressure through line 110 to central bore 78 of spool valve member 76 for the supply of gas to fluid inlet chamber 72. It is noted that the process fluid being sensed through line 62 and inlet sensing chamber 60 is completely isolated and separated from inlet chamber 72, intermediate chamber 104, dome chamber 36, and spool valve 76, and thus can not contaminate these areas. In the normal position of pilot valve 40 as shown in Figures 1 and 2, a fluid pressure differential area is provided within internal bore portion 72 defining the fluid inlet supply chamber and piston 70 is urged in an upward direction opposing the bias of spring 54.
In operation, with a constant pressure exerted by the process fluid in tank 10 against diaphragm 52 in sensing chamber 60, O- ring seals 90 and 96 on spool valve member 76 are seated on adjacent seats 92 and 98. In this position, intermediate fluid chamber 104 and dome chamber 36 are not in communication with fluid inlet chamber 72 or exhaust chamber 102. Upon an increase in the process fluid pressure in tank 10 and inlet sensing chamber 60 a predetermined amount, diaphragm 52 and piston 70 move upwardly to the position shown in Figure 3 to place intermediate fluid chamber 104 in fluid communication with bore 68 and exhaust passage 102 to reduce the pressure in dome chamber 36. Upon exhaust of the auxiliary gas to atmosphere from exhaust chamber 102, the reduced pressure from the auxiliary gas supply acting against piston 70 causes movement of piston 70 downwardly under the bias of spring 54 for seating of seal 96 on seat 98. In the event the process fluid pressure increases again as sensed in sensing chamber 60, piston 70 again moves up to further de-pressurize dome chamber 36. When the pressure in dome chamber 36 decreases an amount so that the opposed forces acting against ends or faces 29 and 34 of unbalanced piston valve member 28 are generally equal, valve member 28 in unseated from seat 36 and opens to permit process pressure from inlet flow passage 24 to flow through valve 14 and outlet flow passage 26 for reducing the pressure in tank 10. If the flow is sufficient to prevent the fluid pressure of the process fluid from increasing, piston 70 will move downwardly under the bias of spring 54 to close the pilot outlet seat 98.
When the fluid pressure of the process fluid decreases in sensing chamber 60 below the set pressure point of pilot valve 40, piston 70 moves downwardly as shown in Figure 4 to provide fluid communication between inlet chamber 72 and dome chamber 36 through line 106 and intermediate chamber 104 thereby to repressurize dome chamber 36. When the pressure in dome chamber 36 increases main valve 28 reseats and an increase in fluid pressure in inlet chamber 72 results in movement of piston 70 upwardly to effect seating of seal 90 on seat 92 thereby blocking fluid communication between inlet chamber 72 and dome chamber 36. It is noted that seal 96 is seated on seat 98 at all times except when the fluid pressure of the process fluid reaches a predetermined high amount in sensing chamber 60. Thus, only a small amount of the supply fluid from fluid source 107 is leaked to atmosphere from exhaust passage 102.
As a specific example, adjustment of pilot valve 40 is made (1) to provide an opening of spool valve member 76 as shown in Figure 3 at a process fluid pressure in sensing chamber 70 above 95% of the set pressure determined by adjustment screw 56, (2) to provide an opening of spool valve member 76 as shown in Figure 4 at a process fluid pressure in sensing chamber 60 below 92% of the set pressure, and (3) to permit spool valve member 76 to remain in a seated position as shown in Figure 2 when the process fluid pressure in sensing chamber 60 is between 92% and 95% of the set pressure. Thus, when the fluid pressure in sensing chamber 60 is below 92% of the set pressure, piston 70 moves downwardly to unseat spool valve member 76 and permit the supply of clean inlet gas to dome chamber 36 through intermediate fluid chamber 104. When the process fluid pressure in sensing chamber 60 increases to 92% of the set pressure, diaphragm 52 and piston 70 are moved upwardly to effect reseating of O-ring seal 90 on seat 92 thereby blocking fluid flow between dome chamber 36 and inlet chamber 72.
In the event fluid pressure of the process fluid increases above 95% of the set pressure, diaphragm 52 and piston 70 move upwardly to unseat spool valve member 76 from seat 98 for exhausting fluid pressure in dome chamber 36 to atmosphere through passage 102. If the process pressure then ceases to increase, piston 70 will move downwardly as a result of the lower dome pressure in chamber 36. In the event fluid process pressure again increases, piston 70 again moves upwardly for unseating of spool valve member 76 from seat 98 to further de-pressurize dome chamber 36. When the dome pressure in chamber 36 decreases to an amount so that fluid pressure acting on opposed faces 29 and 34 main valve member 28 are generally equal, valve member 28 moves upwardly for relief of process fluid through outlet passage 26. If the flow is sufficient to keep the process fluid in sensing chamber 60 from increasing, piston 70 moves downwardly for reseating of spool valve member 76 on seat 98. When the process fluid pressure in sensing chamber 60 decreases below 92% of set point pressure, piston 70 moves downwardly as shown in Figure 4 and dome chamber 36 is re-pressurized by the flow of fluid from inlet supply chamber 72 to dome chamber 36. When the dome pressure in dome chamber 36 increases a predetermined amount, piston 70 moves downwardly for reseating of O-ring seal 90 on seat 92.
As a result of the utilization of a separate auxiliary high pressure fluid, such as nitrogen gas, for the operation of pilot valve 40, spool valve member 76 and dome chamber 36 remain isolated from any process fluid thereby preventing any contamination or malfunctioning thereof resulting from dirty process fluids containing foreign matter. Pilot valve 40 is a non-flowing pilot valve and does not have a continuous fluid flow therethrough during normal operating position. Thus, a very small amount of the auxiliary fluid is exhausted to atmosphere as this occurs only during a drop in fluid pressure of the process fluid below a predetermined amount as shown in Figure 3. Further, in the event regulator 108 develops a leak such as at a seat or the like and pressurizes dome chamber 36 to a pressure above 92% of the set pressure, the set pressure will decrease as a result of the fluid pressure differential area in inlet chamber 72 acting on piston 70 to overcome the downward force of the adjustment spring 54 so that dome chamber 36 is not exhausted to atmosphere as shown in Figure 3. A fluid pressure for the auxiliary gas up to around 3.45 x 10⁷ Pa (5,000 psi) may be provided by the utilization of constant pressure regulator 108 thereby to minimize replenishment of the gas supply in source 107.
While a preferred embodiment of the present invention has been illustrated in detail, it is apparent that modifications an adaptations of the preferred embodiment will occur to those skilled in the art.

Claims

A safety relief system for a pressure vessel having a safety relief valve (14) in a main flow line from the pressure vessel, the safety relief valve including a reciprocable piston type valve member (28) mounted in the flow line in a normally closed position and a dome chamber (36) adjacent an end of the reciprocable valve member;
a pilot valve (40) having a fluid inlet sensing chamber (60) for process fluid from the flow line and a fluid inlet supply chamber (72) for an auxiliary fluid separate from said process fluid;

means (62) providing fluid communication between said main flow line and said fluid inlet sensing chamber;

means (110) to supply an auxiliary fluid to said fluid inlet supply chamber at a predetermined fluid pressure;

a separate fluid chamber (104) in said pilot valve in fluid communication with said dome chamber (36);

an exhaust (102) to atmosphere from said separate fluid chamber;

a movable fluid sensing member (52) in said sensing chamber exposed to said process fluid and responsive to pressure changes in said main flow line;
and

valve means (76) between said separate fluid chamber and said exhaust for normally blocking fluid communication between said separate fluid chamber and said supply chamber;

said valve means being responsive to movement of said fluid sensing member at a predetermined fluid pressure of said process fluid for permitting fluid communication between said separate fluid chamber and said exhaust for reducing fluid pressure in said dome chamber upon the reaching of a predetermined fluid pressure in said process fluid.
A safety relief system according to claim 1 which comprises additional valve means between said fluid inlet supply chamber (72) for said auxiliary fluid supply and said separate fluid chamber (104) normally blocking fluid communication between said separate fluid chamber and said inlet supply chamber;
said valve means being responsive to movement of said fluid sensing member at a predetermined fluid pressure of said process fluid for permitting fluid communication between said fluid supply inlet supply chamber and said separate fluid chamber to provide an auxiliary fluid supply to said separate fluid chamber and said dome chamber (36) at a predetermined pressure reached by said process fluid.
A safety relief system according to claim 1 or 2 in which
said movable fluid sensing member comprises a diaphragm (52) and a piston (70) connected to said diaphragm for movement therewith.
A safety relief system according to claim 3 in which
said valve means comprises a spool valve member (76) responsive to said piston for opening upon a predetermined fluid pressure of said process fluid to permit fluid communication between said dome chamber and said exhaust for reducing fluid pressure in said dome chamber to permit opening of said safety relief valve upon the reaching of a predetermined high fluid pressure in said process fluid.
A method of operating a pilot valve for a control valve in a main flow line in a safety relief system which comprises the following steps;
providing a fluid inlet sensing chamber in the pilot valve in fluid communication with process fluid in the main flow line;

providing a fluid inlet supply chamber in said pilot valve in fluid communication with an auxiliary fluid supply isolated from said process fluid;

providing a source of auxiliary fluid for said fluid inlet supply chamber;

providing an intermediate fluid chamber in fluid communication with a dome chamber in the control valve and in selective fluid communication with said fluid inlet supply chamber;

providing a fluid exhaust chamber in selective fluid communication with said intermediate fluid chamber for reducing the fluid pressure in said dome chamber;
and

providing valving between said intermediate fluid chamber and said exhaust chamber responsive to changes in process fluid pressure in said fluid inlet sensing chamber and blocking fluid communication between said intermediate fluid chamber and said exhaust chamber during normal operation, said valving permitting fluid communication between said intermediate chamber and said exhaust chamber upon the reaching of a predetermined high fluid pressure in said fluid inlet sensing chamber for reducing fluid pressure in said dome chamber.
A method of operating a pilot valve according to claim 5 which further includes the steps of:
providing additional valving betwen said intermediate fluid chamber and said fluid inlet supply chamber responsive to changes in process fluid pressure in said fluid inlet sensing chamber and blocking fluid communication between said intermediate fluid chamber and said fluid inlet supply chamber during normal operation, said additional valving permitting fluid communication between said intermediate chamber and said fluid inlet chamber upon the reaching of a predetermined low fluid pressure in said fluid inlet sensing chamber thereby to provide auxiliary fluid pressure to said dome chamber for said control valve.